Abstract
In this study, the boundary-resistance layer model and soln.-diffusion model were used to investigate the applied driving pressure force technique and the concn. driving force technique, resp., for the prodn. of i.v. drip soln. A 5 kD monolithic membrane coated with Al2O3 and TiO and NaCl aq. soln. as the feed soln. was used. The results show that the boundary-resistance layer model diffusivity coeff., D = 1.8*10-9 m2 sec-1 and the mass transfer coeff., k = 1.19-10-4 m sec-1 which were both slightly higher than the soln.-diffusion model. Applying Fick's law for the soln. diffusion model, the calcd. operating pressure inside the lumen was 15 kPa. Clearly, the findings suggested that the boundary-resistance layer model should be chosen for the prodn. of pure and sterile i.v. salt soln. as it provided higher diffusivity and mass transfer coeff. than the soln.-diffusion model. [on SciFinder (R)]
Original language | English |
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Pages (from-to) | 2069-2075 |
Number of pages | 7 |
Journal | Journal of Applied Sciences |
Volume | 7 |
Issue number | 15 |
Publication status | Published - 2007 |
Keywords
- intravenous salt soln nanofiltration ceramic membrane sterilization
- mass transfer coeff. and osmotic pressure than soln. diffusion model suggesting usefulness of former for prodn. of pure and sterile i.v. salt soln.)
- Permeability (boundary resistance layer model showed higher diffusivity and mass transfer coeff. through ceramic nanofiltration membrane than soln. diffusion model suggesting usefulness of former for prodn. of i.v. salt soln.)
- Osmotic pressure (boundary resistance layer model showed higher diffusivity
- Sterilization and Disinfection (applied pressure driving force technique was useful for prodn. of pure and sterile i.v. salt soln. compared to concn. driving force technique)
- Filtration (nanofiltration
- boundary resistance layer model showed higher diffusivity and mass transfer coeff. through ceramic nanofiltration membrane than soln. diffusion model suggesting usefulness of former for prodn. of i.v. salt soln.)
- Ceramic membranes
- Diffusion
- Mass transfer